CN1238263C - Processing unit for reclaiming dirty oil from united station in oil field - Google Patents

Processing unit for reclaiming dirty oil from united station in oil field Download PDF

Info

Publication number
CN1238263C
CN1238263C CN 200410013673 CN200410013673A CN1238263C CN 1238263 C CN1238263 C CN 1238263C CN 200410013673 CN200410013673 CN 200410013673 CN 200410013673 A CN200410013673 A CN 200410013673A CN 1238263 C CN1238263 C CN 1238263C
Authority
CN
China
Prior art keywords
oil
sediment
lift pump
links
sump oil
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN 200410013673
Other languages
Chinese (zh)
Other versions
CN1562778A (en
Inventor
夏福军
吴迪
陈忠喜
张瑞泉
孟祥春
房永�
罗兴仁
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Daqing Oilfield Co Ltd
Original Assignee
Daqing Oilfield Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Daqing Oilfield Co Ltd filed Critical Daqing Oilfield Co Ltd
Priority to CN 200410013673 priority Critical patent/CN1238263C/en
Publication of CN1562778A publication Critical patent/CN1562778A/en
Application granted granted Critical
Publication of CN1238263C publication Critical patent/CN1238263C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Abstract

The present invention provides a processing device for reclaiming dirty oil from a united station in an oil field, which relates to a processing device for reclaiming dirty oil generated in an oil field. Aiming at the problem of difficult processing existing in dirty oil containing black solid particles in the extracted liquid of the oil field, the present invention provides a processing device for reclaiming dirty oil. The present invention comprises a single-screw rod lifting pump (1) for the dirty oil, a pipeline mixer (2), a three-phase centrifuge (3), a dirty water reclaiming tank (4), a dirty water reclaiming pump (5), a heating and buffering separator (6), a dirty oil lifting pump (7), a solid sediment reclaiming tank (9), a sediment cleaning tank (10) and a lifting pump (11), wherein the pipeline mixer (2) is simultaneously connected with the inlets of the single-screw rod lifting pump (1) and the centrifuge (3); the dirty water outlet of the centrifuge (3) is connected with one end of the dirty water reclaiming tank (4), and the raw oil outlet of the centrifuge (3) is connected with the inlet of the heating and buffering separator (6). The present invention has the characteristics of simple processing technology, good processing effect, flexible operation, convenient transportation, etc., and can be widely used for the production system of the oil field in a matching mode.

Description

Field joint stations sump oil recycling and processing device
Technical field:
The present invention relates to the device that the sump oil that produces in the field joint stations extraction liquid treatment facility is recycled.
Background technology:
In recent years, black solid particulate sump oil has appearred containing in succession in the extraction liquid treatment facility of many oil fields part joint station, wherein at the sewage slurry tank with remove the sump oil on oil tank top, because a large amount of black solid particulate enrichment, caused very big difficulty for extraction liquid and oily water treatment, not only make the water quality deterioration of handling the back oily(waste)water, and can cause the pollution of oil-containing sewage filter and produced-water reinjection system when serious; If the sewage slurry tank and the black solid particulate sump oil that contains that removes the enrichment of oil tank top are recovered to when handling in the dehydrating of crude oil system, excessive layer in the middle of in electrical dehydrator, forming easily, often cause electrical dehydrator to stride electric field, seriously influenced the ordinary production operation of dehydrating of crude oil system.Be normally carrying out of extraction liquid and oily water treatment in the guarantee joint station system, at the sewage slurry tank with remove the sump oil of enrichment in the oil tank and often have to adopt the mode that it is directly effluxed when too much, so not only lose a large amount of crude oil, also caused the serious environmental pollution.This in recent years sump oil recycling problem begins to extend in the joint station in many oil fields, and is the trend that increases the weight of year by year, seriously injures normally carrying out of extraction liquid and oily water treatment production.Therefore, sulfur compound sump oil in the joint station is recycled and controls become in the field produces an important difficult problem anxious to be solved.
Summary of the invention:
The objective of the invention is to contain black colloidal state Iron sulfuret particle sump oil, developed out black colloidal state Iron sulfuret particulate treatment unit in the removing sump oil that is suitable at what formed in the joint station extraction liquid treatment facility.It comprises that sump oil list screw rod lift pump 1, line mixer 2, three-phase separating centrifuge 3, sewage withdrawing can 4, sewage reclaim pump 5, heating surge separator 6, sump oil lift pump 7, solid sediment withdrawing can 9, sediment purge tank 10 and lift pump 11, their mode of connection is: an end of line mixer 2 links to each other with an end of single screw rod lift pump 1, the other end of line mixer 2 links to each other with the inlet of separating centrifuge 3, also is connected with chemicals dosing plant 15 on the line mixer 2; The sewage outlet of separating centrifuge 3 links to each other with an end of sewage withdrawing can 4, and the other end of sewage withdrawing can 4 links to each other with the end that sewage reclaims pump 5, and the other end that sewage reclaims pump 5 connects Sewage treatment systems; The separation slag outlet of separating centrifuge 3 links to each other with an end of solid sediment withdrawing can 9, and the other end of solid sediment withdrawing can 9 links to each other with an end of sediment purge tank 10, and the other end of sediment purge tank 10 links to each other with an end of lift pump 11; The other end of lift pump 11 links to each other with the inlet of separating centrifuge 3, and the liquid in the sediment purge tank 10 promotes through lift pump 11 and enters separating centrifuge 3, outside the sediment drain tank in the sediment purge tank 10; The crude exports of separating centrifuge 3 link to each other with the inlet of heating surge separator 6, the outlet of heating surge separator 6 links to each other with the suction port of sump oil lift pump 7, the other end of sump oil lift pump 7 links to each other with going to the dehydrating of crude oil system by pipeline, below sump oil lift pump 7 and the pipeline that goes to the dehydrating of crude oil system to link to each other branch line being set links to each other with an end of sediment purge tank 10, after sump oil separates in heating surge separator 6, be positioned at the isolated oil of heating surge separator 6 internal upper parts and enter and the pipeline that goes to the dehydrating of crude oil system to link to each other, enter into dehydrating of crude oil system or directly outer defeated by sump oil lift pump 7; Be positioned at the sump oil isolated sewage in below and a small amount of sediment in the heating surge separator, enter sediment purge tank 10 by pipeline and branch line.The present invention is according to the problem that the sump oil recycling that produces in the field joint stations extraction liquid treatment facility is existed; the portable sump oil reclaiming clean treatment unit of developing out; can effectively the black colloidal state Iron sulfuret particle sump oil that contains that produces in the field joint stations extraction liquid treating system facility be purified; black colloidal state Iron sulfuret particle in the sump oil is thoroughly separated from sump oil; avoided the enrichment of the black colloidal state Iron sulfuret particle sump oil that formed in the extraction liquid treating system facility; and be recovered to electro-dewatering and carry out processed and cause the electrical dehydrator electric field that collapses; and then influence the problem of normal production run; the present invention both can be purified the black colloidal state Iron sulfuret particle sump oil that contains that produces in the joint station extraction liquid treatment facility to handle and reclaim; avoided in order to guarantee normal production a large amount of crude oil effluxed environmental pollution and the waste that is caused again; thereby improved the processing efficiency of whole joint station production technique; protected environment; guaranteed the smooth running of dehydrating of crude oil system; improved the dehydration quality of crude oil; and improved re-injection water water quality; make the oily(waste)water re-injection up to standard after the processing and reduced environmental pollution; and guaranteed whole recovery of sump oil and sewage, therefore created good economic benefit and social benefit.In addition because this cover treatment unit system support equipment that is small-sized sled shapeization, it is easy to have a treatment process, and treatment effect is good, flexible operation, and characteristics such as convenient transportation are advanced person's treatment unit comparatively at present, can the extensively supporting oil field development system that is used for.
Description of drawings:
Fig. 1 is a structural representation of the present invention, and Fig. 2 is a structured flowchart of the present invention.
Embodiment:
Embodiment one: present embodiment comprises that sump oil list screw rod lift pump 1, line mixer 2, three-phase separating centrifuge 3, sewage withdrawing can 4, sewage reclaim pump 5, heating surge separator 6, sump oil lift pump 7, solid sediment withdrawing can 9, sediment purge tank 10 and lift pump 11, their mode of connection is: an end of line mixer 2 links to each other with an end of single screw rod lift pump 1, and the other end of line mixer 2 links to each other with the inlet of separating centrifuge 3; The sewage outlet of separating centrifuge 3 links to each other with an end of sewage withdrawing can 4, and the other end of sewage withdrawing can 4 links to each other with the end that sewage reclaims pump 5, and the other end that sewage reclaims pump 5 connects Sewage treatment systems; The separation slag outlet of separating centrifuge 3 links to each other with an end of solid sediment withdrawing can 9, and the other end of solid sediment withdrawing can 9 links to each other with an end of sediment purge tank 10, and the other end of sediment purge tank 10 links to each other with an end of lift pump 11; The other end of lift pump 11 links to each other with the inlet of separating centrifuge 3; The crude exports of separating centrifuge 3 link to each other with the inlet of heating surge separator 6, the outlet of heating surge separator 6 links to each other with the suction port of sump oil lift pump 7, the other end of sump oil lift pump 7 links to each other with going to the dehydrating of crude oil system by pipeline, below sump oil lift pump 7 and the pipeline that goes to the dehydrating of crude oil system to link to each other branch line is set and links to each other with an end of sediment purge tank 10.
Embodiment two: present embodiment and embodiment one difference are, between sewage recovery pump 5 and Sewage treatment systems, under meter 13 is housed, between lift pump 11 and separating centrifuge 3, under meter 12 is housed, at sump oil lift pump 7 and remove to be equipped with between the dehydrating of crude oil system under meter 8, between lift pump 1 and line mixer 2, under meter 14 is housed.
Principle of work of the present invention is: the sump oil that produces in the treatment facility in the field joint stations extraction liquid treating system, behind sump oil list screw rod lift pump 1 and under meter 14, enter line mixer 2, can in line mixer 2, add the sump oil purification agent by chemicals dosing plant 15, carry out oil through entering three-phase separating centrifuge 3 after line mixer 2 mixing, water and black colloidal state Iron sulfuret particle separation, three-phase separating centrifuge 3 isolated sewage enter sewage withdrawing can 4, sewage withdrawing can 4 reclaims pump 5 with sewage and links to each other, and water enters the joint station waste water recovery system through under meter 13 again and does processing again in jar after pump promotes;
Isolated purifying dirty oil enters heating surge separator 6, the purifying dirty oil that enters heating surge separator 6 carries out the short period of time separation of profit by heating, promote through sump oil lift pump 7 then, again via under meter 8, sump oil enters into dehydrating of crude oil system or directly outer defeated by pipeline, below sump oil lift pump 7 and the pipeline that goes to the dehydrating of crude oil system to link to each other, branch line is set, owing to after heating, carried out the separation of profit, promptly entered sediment purge tank 10 so be positioned at the sewage of pipeline below;
Isolated black colloidal state Iron sulfuret particle enters solid sediment withdrawing can 9, isolated black colloidal state Iron sulfuret particle enters sediment purge tank 10 in the solid sediment withdrawing can 9, in jar, add hot water and add clean-out system simultaneously, after stirring and washing, do further separation through lift pump 11 via the ingress that under meter 12 enters three-phase separating centrifuge 3, You Heshui after the separation, repeat said process, and isolated black colloidal state Iron sulfuret particle can utilize again as making the vitriolic starting material.

Claims (5)

1, a kind of field joint stations sump oil recycling and processing device, it comprises sump oil list screw rod lift pump (1), line mixer (2), three-phase separating centrifuge (3), sewage withdrawing can (4), sewage reclaims pump (5), heating surge separator (6), sump oil lift pump (7), solid sediment withdrawing can (9), sediment purge tank (10) and lift pump (11), the mode of connection that it is characterized in that them is: an end of line mixer (2) links to each other with an end of single screw rod lift pump (1), the other end of line mixer (2) links to each other with the inlet of separating centrifuge (3), also is connected with chemicals dosing plant (15) on the line mixer (2); The sewage outlet of separating centrifuge (3) links to each other with an end of sewage withdrawing can (4), and the other end of sewage withdrawing can (4) links to each other with the end that sewage reclaims pump (5), and the other end that sewage reclaims pump (5) connects Sewage treatment systems; The separation slag outlet of separating centrifuge (3) links to each other with an end of solid sediment withdrawing can (9), and the other end of solid sediment withdrawing can (9) links to each other with an end of sediment purge tank (10), and the other end of sediment purge tank (10) links to each other with an end of lift pump (11); The other end of lift pump (11) links to each other with the inlet of separating centrifuge (3), and the liquid in the sediment purge tank (10) promotes through lift pump (11) and enters separating centrifuge (3), outside the sediment drain tank in the sediment purge tank (10); The crude exports of separating centrifuge (3) link to each other with the inlet of heating surge separator (6), the outlet of heating surge separator (6) links to each other with the suction port of sump oil lift pump (7), the other end of sump oil lift pump (7) links to each other with going to the dehydrating of crude oil system by pipeline, with the pipeline below of going to the dehydrating of crude oil system to link to each other branch line being set at sump oil lift pump (7) links to each other with an end of sediment purge tank (10), after sump oil separates in heating surge separator (6), be positioned at the isolated oil of heating surge separator (6) internal upper part and enter and the pipeline that goes to the dehydrating of crude oil system to link to each other, enter into dehydrating of crude oil system or directly outer defeated by sump oil lift pump (7); Be positioned at the sump oil isolated sewage in below and a small amount of sediment in the heating surge separator, enter sediment purge tank (10) by pipeline and branch line.
2, field joint stations sump oil recycling and processing device according to claim 1 is characterized in that between sewage recovery pump (5) and Sewage treatment systems under meter (13) being housed.
3, field joint stations sump oil recycling and processing device according to claim 1 is characterized in that between lift pump (11) and separating centrifuge (3) under meter (12) being housed.
4, field joint stations sump oil recycling and processing device according to claim 1 is characterized in that at sump oil lift pump (7) and removes to be equipped with between the dehydrating of crude oil system under meter (8).
5, field joint stations sump oil recycling and processing device according to claim 1 is characterized in that between lift pump (1) and line mixer (2) under meter (14) being housed.
CN 200410013673 2004-04-09 2004-04-09 Processing unit for reclaiming dirty oil from united station in oil field Expired - Fee Related CN1238263C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200410013673 CN1238263C (en) 2004-04-09 2004-04-09 Processing unit for reclaiming dirty oil from united station in oil field

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200410013673 CN1238263C (en) 2004-04-09 2004-04-09 Processing unit for reclaiming dirty oil from united station in oil field

Publications (2)

Publication Number Publication Date
CN1562778A CN1562778A (en) 2005-01-12
CN1238263C true CN1238263C (en) 2006-01-25

Family

ID=34478240

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200410013673 Expired - Fee Related CN1238263C (en) 2004-04-09 2004-04-09 Processing unit for reclaiming dirty oil from united station in oil field

Country Status (1)

Country Link
CN (1) CN1238263C (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102226099B (en) * 2011-04-12 2013-10-23 大庆油田有限责任公司 Process for recovery and treatment of dirty oil generated in sewage treatment station system
US10722821B2 (en) * 2016-04-08 2020-07-28 Green Flow Industries, LLC Separation and monitoring apparatus
CN107082544A (en) * 2017-06-30 2017-08-22 天津滨海新区东科技发展有限公司 It is a kind of to handle the process that oil stores up cabin bilge oil sludge
CN107952261B (en) * 2017-09-13 2020-05-22 中国石化销售有限公司广东中山石油分公司 Three-head deconcentrator and oil-water separation barrel emptying method
CN109233899B (en) * 2018-09-28 2019-06-18 大庆市地油石油机械有限公司 The environmentally friendly effluent oil recovery device in intelligent oil field operation scene based on PLC system control

Also Published As

Publication number Publication date
CN1562778A (en) 2005-01-12

Similar Documents

Publication Publication Date Title
CN101735851B (en) Recovery and treatment technology of dirty oil produced in sewage setting tank in produced liquid treatment
CN105174577B (en) A kind of coal chemical industrial waste water pretreating process and device
CN109052688A (en) A kind of sandstone wastewater processing system and method
CN106186255A (en) A kind of board-like Magneto separate sewage disposal system
CN108358286A (en) A kind of magnetic flocculation urban rainwater processing unit and its technique
CN201793456U (en) Oily sewage treatment system
CN1238263C (en) Processing unit for reclaiming dirty oil from united station in oil field
CN207356646U (en) A kind of skid-mounted type integrated oil field filtering oily sewage tank filtering material cleaning device
CN101386790B (en) Ground crude oil dewatering treater
CN103224299A (en) Oily sewage oil-skimming and deslagging system
CN202729934U (en) Collecting and reusing system for glass edge polishing waste water
CN102282237A (en) Heavy hydrocarbon removal systems and methods
CN110540331A (en) process method for removing oil and reducing COD (chemical oxygen demand) of wastewater by using hexamethyl silazane
CN205241402U (en) A sewage treatment system for concrete mixing plant
CN101823784A (en) Method for purifying sewage quickly by nano material and device thereof
CN209507962U (en) A kind of dangerous waste processing pumping system
CN205821023U (en) Oil recovery system in a kind of raising oily sludge waste water
CN217323454U (en) Medium oil removing filter
CN106191890A (en) Strip cleaning liquid recycling plant and strip cleaning liquid circulation process method
CN105884069B (en) Oil recovery method and system in a kind of raising oily sludge waste water
CN204981243U (en) A membrane sediment treatment facility for PCB shells membrane equipment
CN109467214A (en) A kind of vehicle-mounted renewable resource mimicry reduction apparatus
CN109133427A (en) A kind of wastewater from car washer processing system
CN104649446A (en) Liquid-solid separation method and device for MTO (methanol to olefins) quenching water and washing water
CN217709328U (en) Heavy dirty oil ultrasonic treatment device

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee